Mass transfer in packed beds of screens

Experimental and theoretical work on mass transfer to gauzes was carried out. Mass transfer rates were measured by the electrochemical method using one, three, six and nine wire screens. Models representing the packed bed of screens as an assemblage of circular cylinders in cross flow or as a bundle...

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Detalles Bibliográficos
Autores principales: Cano, J., Böhm, U.
Formato: JOUR
Materias:
CATALYSIS
HEAT TRANSFER
MASS TRANSFER
Acceso en línea:http://hdl.handle.net/20.500.12110/paper_00092509_v32_n2_p213_Cano
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Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA) de Universidad de Buenos Aires
id todo:paper_00092509_v32_n2_p213_Cano
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spelling todo:paper_00092509_v32_n2_p213_Cano2023-10-03T14:08:02Z Mass transfer in packed beds of screens Cano, J. Böhm, U. CATALYSIS HEAT TRANSFER MASS TRANSFER Experimental and theoretical work on mass transfer to gauzes was carried out. Mass transfer rates were measured by the electrochemical method using one, three, six and nine wire screens. Models representing the packed bed of screens as an assemblage of circular cylinders in cross flow or as a bundle of square ducts, were developed. The experimental data of this and other works were correlated as j/Z vs Re and j. E/(D/d)1 3 vs Ret′, parameters obtained from the theoretical models, which showed to improve the correlation of data with respect to usual empirical relationships. © 1977. JOUR info:eu-repo/semantics/openAccess http://creativecommons.org/licenses/by/2.5/ar http://hdl.handle.net/20.500.12110/paper_00092509_v32_n2_p213_Cano
institution Universidad de Buenos Aires
institution_str I-28
repository_str R-134
collection Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA)
topic CATALYSIS
HEAT TRANSFER
MASS TRANSFER
spellingShingle CATALYSIS
HEAT TRANSFER
MASS TRANSFER
Cano, J.
Böhm, U.
Mass transfer in packed beds of screens
topic_facet CATALYSIS
HEAT TRANSFER
MASS TRANSFER
description Experimental and theoretical work on mass transfer to gauzes was carried out. Mass transfer rates were measured by the electrochemical method using one, three, six and nine wire screens. Models representing the packed bed of screens as an assemblage of circular cylinders in cross flow or as a bundle of square ducts, were developed. The experimental data of this and other works were correlated as j/Z vs Re and j. E/(D/d)1 3 vs Ret′, parameters obtained from the theoretical models, which showed to improve the correlation of data with respect to usual empirical relationships. © 1977.
format JOUR
author Cano, J.
Böhm, U.
author_facet Cano, J.
Böhm, U.
author_sort Cano, J.
title Mass transfer in packed beds of screens
title_short Mass transfer in packed beds of screens
title_full Mass transfer in packed beds of screens
title_fullStr Mass transfer in packed beds of screens
title_full_unstemmed Mass transfer in packed beds of screens
title_sort mass transfer in packed beds of screens
url http://hdl.handle.net/20.500.12110/paper_00092509_v32_n2_p213_Cano
work_keys_str_mv AT canoj masstransferinpackedbedsofscreens
AT bohmu masstransferinpackedbedsofscreens
_version_ 1807317684146143232

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